EP0076549A1 - Produit à tartiner à faible teneur en matières grasses et procédé pour sa fabrication - Google Patents

Produit à tartiner à faible teneur en matières grasses et procédé pour sa fabrication Download PDF

Info

Publication number
EP0076549A1
EP0076549A1 EP82201220A EP82201220A EP0076549A1 EP 0076549 A1 EP0076549 A1 EP 0076549A1 EP 82201220 A EP82201220 A EP 82201220A EP 82201220 A EP82201220 A EP 82201220A EP 0076549 A1 EP0076549 A1 EP 0076549A1
Authority
EP
European Patent Office
Prior art keywords
cream
process according
oil
spread
fat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP82201220A
Other languages
German (de)
English (en)
Other versions
EP0076549B1 (fr
Inventor
David Patrick Joseph Moran
David George Sharp
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unilever PLC
Unilever NV
Original Assignee
Unilever PLC
Unilever NV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unilever PLC, Unilever NV filed Critical Unilever PLC
Priority to AT82201220T priority Critical patent/ATE12338T1/de
Publication of EP0076549A1 publication Critical patent/EP0076549A1/fr
Application granted granted Critical
Publication of EP0076549B1 publication Critical patent/EP0076549B1/fr
Expired legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D7/00Edible oil or fat compositions containing an aqueous phase, e.g. margarines
    • A23D7/02Edible oil or fat compositions containing an aqueous phase, e.g. margarines characterised by the production or working-up
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D7/00Edible oil or fat compositions containing an aqueous phase, e.g. margarines
    • A23D7/015Reducing calorie content; Reducing fat content, e.g. "halvarines"

Definitions

  • the present invention relates to an oil-in-water-in-oil emulsion (o/w/o emulsion) containing less than 80% fat, particularly a low calorie spread with a level of fat ranging from 20 to 60%, and ideally from 30-50%.
  • An o/w/o emulsion is an emulsion in which the continuous phase is an oil or fat (these terms are meant to be interchangeable throughout the specification) and the dispersed phase consists of a natural or an artificial cream.
  • the main object of the present invention is to produce an o/w/o emulsion which on consumption- gives a creamy sensation and a good flavour impact on the palate.
  • the fat spread with a level of fat ranging from 20 to 60% according to the invention comprises :
  • whey protein allows the preparation of emulsions having an aqueous phase of a relatively low pH, i.e. a pH ranging from 3.5 to 5.5, which promotes bacteriological stability, without recourse to a protein-complexing agent, such as carboxy methyl cellulose or to a slow culturing procedure to avoid precipitation of the protein.
  • whey protein stabilized the cream at relatively low levels, i.e. at levels ranging from 0.1 to 2 wt.%, based on the total fat composition, in contrast to the much higher levels of milk protein emsulsifier advocated in Dutch patent application N° 650,380 for the stabilization of o/w/o emulsions.
  • whey protein used in the whey protein. It is therefore useful that the whey protein used is substantially free from other milk proteins such as casein.
  • the spreads according to the invention preferably contain a whey protein which has been obtained by membrane filtration of whey to remove low molecular components such as sugars, particularly lactose, which give an undesirable, sweet impression on consumption.
  • the whey protein used in the spreads according to the invention is denatured by a heat treatment carried out at a temperature ranging from 80 to 95°C.
  • the cream may further contain viscosity increasing agents or a gelling agent such as gelatin, starch, carboxymethyl cellulose, locust bean gum, carrageenan or mixtures thereof, at a level ranging from 0.05 to 5 wt.%.
  • viscosity increasing agents such as gelatin, starch, carboxymethyl cellulose, locust bean gum, carrageenan or mixtures thereof, at a level ranging from 0.05 to 5 wt.%.
  • gelatin is used because of its melting behaviour under conditions prevailing in the mouth, at a level preferably exceeding 1%.
  • the continous fat phase of the emulsion contains an emulsifier or a mixture of emulsifiers.
  • an emulsifier or a mixture of emulsifiers.
  • a mixture of a phospholipid such as lecithin and a partial glyceride is used.
  • the weight ratio of the oil present in the dispersed phase of the emulsion to the oil used in the continuous fatty phase ranges from 0.1 to 0.5 and preferably from 0.2 to 0.4.
  • a cream is produced which contains less than 15 wt.% of oil, based on the total composition.
  • Various fats and oils can be present in the continuous and dispersed phases. When a relatively high amount of fat is present in the dispersed phase, some leakage may occur. In that case it is preferred that the same oil or fat be used in both cases to prevent any leakage from affecting the properties of the final product.
  • oils displaying a steep dilatation line such as palmkernel oil, coconut oil or babassu oil, are preferably present in the cream to impart coolness to the product on consumption.
  • these fats are present as partially or wholly hydrogenated fats, they may achieve an enhanced creamy sensation on the palate.
  • the fat of the continuous phase consists generally of a plastic fat blend which may contain vegetable or animal fats or fractions thereof, part of which may have been hydrogenated or interesterified to achieve specific melting properties.
  • the process according to the invention for producing low calorie spreads having a level of fat ranging from 20-60%, preferably 30-50%, comprises :
  • the protein used for producing the cream be present in the native, undenatured state in the initial stage of the process.
  • a whey protein is used which has been obtained by membrane filtration.
  • the temperature is raised to above 80°C and preferably from 85 to 95°C, e.g. for 20 to 40 minutes, to denature the protein.
  • This heat treatment raises the viscosity of the emulsion/cream, increases the stabilization of the o/w interface and by desolubilization decreases the tendency of the protein not at the o/w interface to destabilize the final cream in the fat spread.
  • the fine dispersion of oil (0.1-2 microns) in the cream is achieved by subjecting a mixture of the whey protein, water and oil to homogenization under a pressure ranging from 100-400 kg/cm 2 at a temperature higher than the temperature at which the oil starts melting.
  • a second homogenization step is carried out subsequent to step (ii) and prior to step (iii) to thoroughly reduce clumps of denatured protein and fat aggregates.
  • the fat which constitutes the continuous phase of the emulsion is first fed into a rotating emulsification unit, whereafter the cream is proportioned to obtain a w/o- emulsion, which is subsequently subjected to cooling and texturizing treatments to plasticize the emulsion.
  • Cooling and texturizing can be carried out in Votator, Perfector, Kombinator or Complector apparatus.
  • Whey protein (1.66%) obtained by membrane filtration was dissolved in water (37 wt.%) at 60°C.
  • a fat blend (7.5. wt.%) at 60°C, containing flavour, was added to the protein solution and the mixture was subjected to high pressure homogenization at 250 kg/cm 2 to produce a cream in which the average size of the droplets was about 1 micron.
  • Gelatin 1.5 wt.%, dissolved in water (15 wt.%), was added to the cream. Further water was added to reach a level of 55.5 wt.%. The pH was adjusted to 4.7, using a 20% solution of lactic acid, and water-soluble flavours (0.1 wt.%) were added.
  • the cream was pasteurized at 90°C for 30 minutes to denature the whey protein. In order to disperse possible clumps, the cream was re- homogenized at a pressure of 70 kg/cm 2 .
  • the fat-continuous emulsion emerging from the C-unit was processed through a Votator sequence ACAC to obtain the final fat-continuous spread.
  • Example 1 The procedure of Example 1 was repeated, except that the level of gelatin was increased to the following concentrations : 2.5%, 5%.
  • the Instron test values on the gel, the flavour impact scores and the creaminess scores are summarized in Tables A and B.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Edible Oils And Fats (AREA)
  • Grain Derivatives (AREA)
  • Dairy Products (AREA)
EP82201220A 1981-10-07 1982-09-30 Produit à tartiner à faible teneur en matières grasses et procédé pour sa fabrication Expired EP0076549B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82201220T ATE12338T1 (de) 1981-10-07 1982-09-30 Fettarmer brotaufstrich und verfahren zur herstellung desselben.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8130323 1981-10-07
GB8130323 1981-10-07

Publications (2)

Publication Number Publication Date
EP0076549A1 true EP0076549A1 (fr) 1983-04-13
EP0076549B1 EP0076549B1 (fr) 1985-03-27

Family

ID=10525009

Family Applications (1)

Application Number Title Priority Date Filing Date
EP82201220A Expired EP0076549B1 (fr) 1981-10-07 1982-09-30 Produit à tartiner à faible teneur en matières grasses et procédé pour sa fabrication

Country Status (8)

Country Link
US (1) US4515825A (fr)
EP (1) EP0076549B1 (fr)
JP (1) JPS5871844A (fr)
AT (1) ATE12338T1 (fr)
AU (1) AU548795B2 (fr)
CA (1) CA1190431A (fr)
DE (1) DE3262809D1 (fr)
ZA (1) ZA827303B (fr)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4614656A (en) * 1984-05-14 1986-09-30 Lever Brothers Company Two phase margarine
US4671966A (en) * 1984-07-30 1987-06-09 Battelle Memorial Institute Method for fabricating a thickener concentrate for thickening sauces
EP0244009A2 (fr) * 1986-04-28 1987-11-04 Unilever N.V. Matières à tartiner
EP0353798A2 (fr) * 1988-07-18 1990-02-07 Unilever N.V. Traitement de gélifiants
EP0355058A2 (fr) * 1988-08-16 1990-02-21 Unilever Plc Produit alimentaire
EP0369550A2 (fr) * 1988-11-18 1990-05-23 Unilever N.V. Produits à tartiner
EP0496466A2 (fr) * 1991-01-23 1992-07-29 Unilever N.V. Matière à tartiner comestible
WO1992018239A1 (fr) 1991-04-23 1992-10-29 Kenneth Herbert Rhodes Procede de preparation d'un succedane de matiere grasse derive de lactoserum
GB2255489A (en) * 1991-01-14 1992-11-11 St Ivel Ltd Process for making a vegetable fat cream and cheese product therefrom
US5188842A (en) * 1988-06-16 1993-02-23 Van Den Bergh Foods Co., Division Of Conopco, Inc. Edible plastic compositions
EP0603981A1 (fr) * 1992-12-23 1994-06-29 Verenigde Coöperatieve Melkindustrie Coberco B.A. Procédé de préparation d'une émulsion dont la viscosité est ajustable; l'émulsion ainsi préparée et aliment obtenu en utilisant cette émulsion
EP0603980A1 (fr) * 1992-12-23 1994-06-29 Verenigde Coöperatieve Melkindustrie Coberco B.A. Procédé pour préparer une émulsion dont la viscosité est ajustable
US6136364A (en) * 1994-09-08 2000-10-24 Kraft Foods, Inc. Microcapsule flavor delivery system

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4546003A (en) * 1982-07-28 1985-10-08 Lever Brothers Company Edible composition comprising discrete fat-bearing particles in a fat-bearing matrix
US5098728A (en) 1989-06-16 1992-03-24 John Labatt Limited/John Labbat Limitee Reduced fat food product
US5102681A (en) 1984-05-04 1992-04-07 John Labatt Limited/John Labatt Limitee Reduced fat salad dressing
US4734287A (en) 1986-06-20 1988-03-29 John Labatt Limited Protein product base
US4961953A (en) 1986-06-20 1990-10-09 John Labatt Limited/John Labatt Limitee Fat emulating protein products and process
US5139811A (en) 1984-05-04 1992-08-18 John Labatt Limited Viscous salad dressing
CH662707A5 (fr) * 1985-03-19 1987-10-30 Nestle Sa Preparation de produits alimentaires gelifies.
US4917915A (en) * 1986-03-06 1990-04-17 Lever Brothers Company Water-in-oil emulsion spread
US5096730A (en) 1986-06-20 1992-03-17 John Labatt Limited/John Labatt Limitee Reduced fat sour cream
US4820541A (en) * 1987-04-16 1989-04-11 Lever Brothers Company Spread containing dairy fat
US4978553A (en) * 1987-11-02 1990-12-18 Jules Silver Method of making low-fat butter or margarine spread and resulting product
US4849243A (en) * 1987-12-21 1989-07-18 Lever Brothers Company Process for producing low fat spreads by phase inversion
DE3913125A1 (de) * 1988-05-31 1989-12-14 Maroudas Johann Verfahren zur herstellung eines nahrungsmittels
US5021248A (en) * 1988-09-19 1991-06-04 Enzytech, Inc. Hydrophobic protein microparticles and preparation thereof
US5096731A (en) 1989-06-16 1992-03-17 John Labatt Limited/John Labatt Limitee Reduced fat yogurt
US5104679A (en) * 1989-07-11 1992-04-14 The Clorox Company Dressing or marinade of the multiple-phase separating type
US5080921A (en) * 1990-02-05 1992-01-14 Pfizer Inc. Low calorie fat substitute
US5120561A (en) * 1991-04-25 1992-06-09 American Lecithin Company Food composition and method
CA2407307A1 (fr) * 2000-04-20 2001-11-01 University Of Guelph Processus de preparation de margarine a teneur en huile liquide elevee
BR0107086A (pt) * 2000-08-11 2002-06-18 Novozymes North America Inc Processo para produzir um aditivo para produto lácteo, aditivo para produto lácteo, processo para produzir um produto lácteo, e, produto lácteo
US7314045B2 (en) * 2001-07-26 2008-01-01 Tru-Fire Corporation Bow string release having floating jaws and a trigger force adjustment mechanism
SI1677613T1 (sl) 2003-10-30 2012-11-30 Arla Foods Amba Stabilizatorji uporabni pri izdelavi namazov z nizko vsebnostjo maščob
US20070048431A1 (en) * 2005-08-31 2007-03-01 Budwig Christopher E Emulsions for confectionery applications
US7927646B2 (en) * 2006-11-03 2011-04-19 Land O'lakes, Inc. Refrigeration-temperature spreadable butter-based product
JP5128982B2 (ja) * 2008-02-21 2013-01-23 株式会社Adeka 油中水型クリーム
JP6002491B2 (ja) * 2012-07-27 2016-10-05 ミヨシ油脂株式会社 二重乳化油脂組成物の製造方法

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1023781A (fr) * 1950-08-25 1953-03-24 Procédé de fabrication de crème et produit obtenu par ce procédé
DE1492955A1 (de) * 1964-03-25 1970-01-15 Unilever Nv Verfahren zur Herstellung von Speisefettmischungen

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3729325A (en) * 1971-07-07 1973-04-24 Procter & Gamble Process for forming a stable oil and water-soluble protein-containing emulsion and product thereof
GB1440181A (en) * 1972-05-18 1976-06-23 Unilever Ltd Food compositions
US3892873A (en) * 1973-11-19 1975-07-01 Kraftco Corp Emulsified oil dressing
US3892039A (en) * 1974-01-21 1975-07-01 Fred W Fisher Compound removal tool
GB1564400A (en) * 1975-11-07 1980-04-10 Unilever Ltd Proteinaceous low fat spread
JPS55120745A (en) * 1979-03-09 1980-09-17 Asahi Denka Kogyo Kk Oil-in-water-in-oil type double emulsified oil composition
NL8002925A (nl) * 1980-05-21 1981-12-16 Unilever Nv Werkwijze ter bereiding van vetarme olie-in-water-in-olie emulsies.
ATE9430T1 (de) * 1980-11-27 1984-10-15 Unilever Nv Verfahren zur herstellung einer kontinuierlichen fettemulsion, bestehend aus einer fettmischung mit hohem gehalt an festem fett bei verhaeltnismaessig hohen umgebungstemperaturen.

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1023781A (fr) * 1950-08-25 1953-03-24 Procédé de fabrication de crème et produit obtenu par ce procédé
DE1492955A1 (de) * 1964-03-25 1970-01-15 Unilever Nv Verfahren zur Herstellung von Speisefettmischungen

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4614656A (en) * 1984-05-14 1986-09-30 Lever Brothers Company Two phase margarine
US4671966A (en) * 1984-07-30 1987-06-09 Battelle Memorial Institute Method for fabricating a thickener concentrate for thickening sauces
EP0244009A2 (fr) * 1986-04-28 1987-11-04 Unilever N.V. Matières à tartiner
EP0244009A3 (en) * 1986-04-28 1988-01-07 Unilever Nv Spreads
US5188842A (en) * 1988-06-16 1993-02-23 Van Den Bergh Foods Co., Division Of Conopco, Inc. Edible plastic compositions
AU615085B2 (en) * 1988-07-18 1991-09-19 Unilever Plc Treatment of gelling agents
EP0353798A2 (fr) * 1988-07-18 1990-02-07 Unilever N.V. Traitement de gélifiants
EP0353798A3 (en) * 1988-07-18 1990-11-07 Unilever Nv Treatment of gelling agents
US5145704A (en) * 1988-07-18 1992-09-08 Van Den Bergh Foods Co., Division Of Conopco, Inc. Method of preparing an emulsion spread using a wet gelatine retentate
EP0355058A2 (fr) * 1988-08-16 1990-02-21 Unilever Plc Produit alimentaire
EP0355058A3 (fr) * 1988-08-16 1991-01-09 Unilever Plc Produit alimentaire
EP0369550A2 (fr) * 1988-11-18 1990-05-23 Unilever N.V. Produits à tartiner
EP0369550A3 (fr) * 1988-11-18 1991-08-14 Unilever N.V. Produits à tartiner
GB2255489A (en) * 1991-01-14 1992-11-11 St Ivel Ltd Process for making a vegetable fat cream and cheese product therefrom
GB2255489B (en) * 1991-01-14 1994-10-19 St Ivel Ltd Process for making a vegetable fat cream and cheese product therefrom
EP0496466A3 (fr) * 1991-01-23 1992-08-19 Unilever N.V. Matière à tartiner comestible
EP0496466A2 (fr) * 1991-01-23 1992-07-29 Unilever N.V. Matière à tartiner comestible
US5656322A (en) * 1991-01-23 1997-08-12 Van Den Bergh Foods Co., Division Of Conopco Inc. Edible spread with aqueous phase with non-gelling thickener system and low protein content
WO1992018239A1 (fr) 1991-04-23 1992-10-29 Kenneth Herbert Rhodes Procede de preparation d'un succedane de matiere grasse derive de lactoserum
US5413804A (en) * 1991-04-23 1995-05-09 Cacique, Inc. Process for making whey-derived fat substitute product and products thereof
EP0603981A1 (fr) * 1992-12-23 1994-06-29 Verenigde Coöperatieve Melkindustrie Coberco B.A. Procédé de préparation d'une émulsion dont la viscosité est ajustable; l'émulsion ainsi préparée et aliment obtenu en utilisant cette émulsion
EP0603980A1 (fr) * 1992-12-23 1994-06-29 Verenigde Coöperatieve Melkindustrie Coberco B.A. Procédé pour préparer une émulsion dont la viscosité est ajustable
US6136364A (en) * 1994-09-08 2000-10-24 Kraft Foods, Inc. Microcapsule flavor delivery system

Also Published As

Publication number Publication date
ATE12338T1 (de) 1985-04-15
AU8899582A (en) 1984-04-12
JPS6217495B2 (fr) 1987-04-17
AU548795B2 (en) 1986-01-02
ZA827303B (en) 1984-05-30
CA1190431A (fr) 1985-07-16
US4515825A (en) 1985-05-07
JPS5871844A (ja) 1983-04-28
EP0076549B1 (fr) 1985-03-27
DE3262809D1 (en) 1985-05-02

Similar Documents

Publication Publication Date Title
US4515825A (en) Low fat spread and process for producing same
EP0455288B1 (fr) Crème à fouetter non laitière
US4513017A (en) Process for producing a spread starting from a bimodal dispersed phase
EP0011891A1 (fr) Emulsions et procédé pour leur préparation
US5217742A (en) Water-and-oil emulsion and process for preparing such emulsion
EP0011344A1 (fr) Emulsion eau dans l'huile
EP0387940B1 (fr) Produit à tartiner
CA2128200C (fr) Procede de fabrication de tartinades et tartinades obtenues au moyen dudit procede
CA1169700A (fr) Procede de production d'une emulsion d'huile dans l'eau dans l'huile a faible teneur en matiere grasse
EP0420314A2 (fr) Produit à tartiner
US4362758A (en) Process for producing a low-calorie spread
CA1169290A (fr) Procede de production d'une emulsion homogene de matieres grasses comprenant un melange de matieres grasses riche en matiere solide a des temperatures ambiantes relativement elevees
GB2084171A (en) Process for producing a low- calorie spread
US3366492A (en) Process for making low fat spread
EP0480531B1 (fr) Procédé de préparation d'un produit à tartiner contenant de la lactoprotéine et/ou protéine végétable ainsi qu'un agent épaississant et une installation apte à être utilisée dans ce procédé
EP0540086A1 (fr) Crème à fouetter non-laitière à faible teneur en matières grasses
US6171637B1 (en) Inversion process for making fat continuous spreads
EP0356094A2 (fr) Produit alimentaire
EP0355058A2 (fr) Produit alimentaire
EP0393739B1 (fr) Beurres à tartiner
JPH0771460B2 (ja) 霜降り肉とその製造方法
GB2225696A (en) Low fat spread
JPS6214257B2 (fr)
JPH0362387B2 (fr)

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI LU NL SE

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: UNILEVER PLC

Owner name: UNILEVER NV

17P Request for examination filed

Effective date: 19830422

R17P Request for examination filed (corrected)

Effective date: 19830422

ITF It: translation for a ep patent filed

Owner name: JACOBACCI & PERANI S.P.A.

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI LU NL SE

REF Corresponds to:

Ref document number: 12338

Country of ref document: AT

Date of ref document: 19850415

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3262809

Country of ref document: DE

Date of ref document: 19850502

ET Fr: translation filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19850916

Year of fee payment: 4

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19850930

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Effective date: 19860930

Ref country code: CH

Effective date: 19860930

Ref country code: AT

Effective date: 19860930

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

EAL Se: european patent in force in sweden

Ref document number: 82201220.9

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20010813

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20010817

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20010820

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20010830

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20010917

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20010920

Year of fee payment: 20

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20020929

BE20 Be: patent expired

Owner name: *UNILEVER N.V.

Effective date: 20020930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20020930

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Effective date: 20020929

EUG Se: european patent has lapsed

Ref document number: 82201220.9

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20020930